US5061745A - Flame-retardant, high-impact polycarbonate molding compounds - Google Patents
Flame-retardant, high-impact polycarbonate molding compounds Download PDFInfo
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- US5061745A US5061745A US07/355,957 US35595789A US5061745A US 5061745 A US5061745 A US 5061745A US 35595789 A US35595789 A US 35595789A US 5061745 A US5061745 A US 5061745A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/49—Phosphorus-containing compounds
- C08K5/51—Phosphorus bound to oxygen
- C08K5/52—Phosphorus bound to oxygen only
- C08K5/521—Esters of phosphoric acids, e.g. of H3PO4
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/49—Phosphorus-containing compounds
- C08K5/51—Phosphorus bound to oxygen
- C08K5/53—Phosphorus bound to oxygen bound to oxygen and to carbon only
- C08K5/5317—Phosphonic compounds, e.g. R—P(:O)(OR')2
- C08K5/5333—Esters of phosphonic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates
Definitions
- This invention relates to high-impact, flame-retardant, thermoplastic polycarbonate molding compounds consisting of
- thermoplastic, halogen-free, aromatic polycarbonates based on diphenols corresponding to formula (II),
- B.2 95 to 10 parts by weight, preferably 70 to 20 parts by weight, based on B), of a rubber having a glass temperature T G of ⁇ 10° C.
- component E) 0.05 to 5 parts by weight, preferably 0.1 to 1 part by weight and, more preferably, 0.1 to 0.5 part by weight, based on 100 parts by weight of A)+B)+optionally C), of a tetrafluoroethylene polymer having average particle sizes of from 0.05 to 1000 ⁇ m, a density of 1.2 to 2.3 g/cm 3 and a fluorine content of 65 to 76% by weight, component E) preferably being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) having an average particle size of 0.05 to 20 ⁇ and a density of 1.2 to 1.9 g/cm 3 with emulsions of graft polymers B) and the ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) being from 95:5 to 60:40 and the content of addition quantities B), based on 100 parts by weight A)+B) and optionally C), being from 0.1 to
- DE-OS 3 322 260 (Le A 22 391) describes flame-retardant thermoplastic molding compounds of
- thermoplastic polymer 0 to 50 parts by weight of a thermoplastic polymer
- DE-OS 3 430 234 (Le A 22 925) describes flame-resistant thermoplastic polymer mixtures containing special, halogen-free polycarbonates of 50 mol % to 100 mol % tetraalkylated bisphenol carbonate structural units, halogen-free styrene polymers and/or halogen-free graft polymers, halogen-free phosphate esters and, optionally, tetrafluoroethylene polymers.
- EP-OS 0 174 493 (Le A 23 043-EP) describes thermoplastic molding compounds consisting of
- thermoplastic aromatic polycarbonate A) 20 to 85 parts by weight of a thermoplastic aromatic polycarbonate
- DE-OS 3 521 388 (Le A 23 877) describes thermoplastic flame-resistant molding compounds containing halogen-free polycarbonates, copolymers of styrenes with maleic anhydride, phosph(on)ate esters, tetrafluoroethylene polymers and 0.1 to 3 parts by weight graft polymers, the graft polymers again having been co-precipitated with the tetrafluoroethylene polymers.
- these molding compounds achieve a V-O rating for a thickness of 1.6 mm, their toughness, flow line strength and resistance to stress crazing are inadequate for numerous applications.
- DE-OS 3 523 314 (Le A 23 940) describes high-impact, flame-retardant molding compounds of halogen-free polycarbonates, halogen-free styrene-acrylonitrile copolymers, phosphorus compounds, tetrafluoroethylene polymers and 0.1 to 3 parts by weight graft polymers, the graft polymers again having been co-precipitated with the tetrafluoroethylene polymers.
- the toughness, flow line strength and resistance to stress crazing of the molding compounds according to DE-OS 3 523 314 is inadequate for certain applications, particularly in the case of complicated, flame-proofed moldings, such as housing components, where design-related openings, webs and the like call for as high a level of the above-mentioned properties as possible.
- thermoplastic, halogen-free aromatic polycarbonate A) 40 to 95 parts by weight, based on 100 parts by weight A)+B)+C), of a thermoplastic, halogen-free aromatic polycarbonate,
- F stabilizers, pigments, flow aids, mold release agents and/or antistatic agents.
- molding compounds of the type in question have the disadvantage of a narrower processing scope and lower flow line strength than the molding compounds according to the invention.
- DE-OS 3 628 904 (Le A 24 683) describes high-impact flame-retardant polycarbonate molding compounds consisting of
- DE-OS 3 629 546 (Le-A 24 695) describes high-impact flame-retardant molding compounds containing
- component D) being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers D) with emulsions of at most 3 parts by weight, but at least 0.1 part by weight, based on 100 parts by weight of the sum of components A) and B), of graft polymers
- the technical advantage of the molding compounds according to the invention lies in the extremely advantageous combination of toughness, resistance to stress crazing and flame resistance, the latter being achieved without any halogen (Br, Cl) and metal compounds.
- Thermoplastic, halogen-free, aromatic polycarbonates of component A) suitable for use in accordance with the invention are those based on diphenols corresponding to formula (II) ##STR6## in which A is a single bond, C 1 -C 5 alkylene, C 2 -C 5 alkylidene, C 5 -C 6 cycloalkylidene, --S-- or --SO 2 --.
- Suitable diphenols corresponding to formula (II) are, for example, hydroquinone, resorcinol, 4,4'-dihydroxydiphenyl, 2,2-bis-(4-hydroxyphenyl)-propane, 2,4-bis-(4-hydroxyphenyl)-2-methyl butane or 1,1-bis-(4-hydroxyphenyl)cyclohexane.
- Preferred diphenols corresponding to formula (II) are 2,2-bis-(4-hydroxyphenyl)-propane and 1,1-bis-(4-hydroxyphenyl)-cyclohexane.
- diphenols corresponding to formula (II) are either known from the literature or may be produced by methods known from the literature.
- polycarbonates of component A) suitable for use in accordance with the invention is known from the literature and may be carried out, for example, with phosgene by the interfacial process or with phosgene by the homogeneous-phase process (so-called pyridine process), the particular molecular weight to be established being obtained in known manner through a corresponding quantity of known chain terminators.
- Suitable chain terminators are, for example, monophenols, such as phenol itself, p-cresol, p-tert.-butylphenol and p-isooctylphenol.
- the polycarbonates of component A) suitable for use in accordance with the invention have average molecular weights (M w , as measured for example by ultracentrifugation or by scattered light measurement) of from 10,000 to 200,000 and preferably from 20,000 to 80,000.
- polycarbonates of component A) suitable for use in accordance with the invention are both homopolycarbonates and also copolycarbonates.
- polycarbonates of component A) suitable for use in accordance with the invention may be branched in known manner, preferably through the incorporation of 0.05 to 2.0 mol %, based on the sum of the diphenols used, of trifunctional or more than trifunctional compounds, for example those containing three or more than three phenolic OH groups.
- halogen-free polycarbonates are understood to be polycarbonates of halogen-free diphenols, halogen-free chain terminators and, optionally, halogen-free branching agents, the content of small quantities (ppm) of hydrolyzable chlorine, resulting for example from the production of the polycarbonates with phosgene by the interfacial process, not counting as "halogen-containing" in the context of the invention.
- Polycarbonates such as these having ppm contents of hydrolyzable chlorine are halogen-free polycarbonates in the context of the invention.
- Rubbers suitable for the production of the halogen-free graft polymers B) are, in particular, polybutadiene, butadiene/styrene copolymers (both also copolymerized with up to 30% by weight, based on the weight of the rubber, of a lower alkyl ester of acrylic or methacrylic acid, such as methyl methacrylate, ethyl acrylate, methyl acrylate or ethyl methacrylate), polyisoprene, alkyl acrylate rubbers (of C 1 -C 8 alkyl acrylates, particularly ethyl, butyl, ethyl hexyl acrylate).
- the alkyl acrylate rubbers may optionally contain up to 30% by weight, based on the weight of the rubber, of such monomers as vinyl acetate, acrylonitrile, styrene, methyl methacrylate and/or vinyl ethers in copolymerized form and also relatively small quantities, preferably up to 5% by weight, based on the weight of the rubber, of crosslinking, ethylenically unsaturated monomers.
- Crosslinking agents such as these are, for example, alkylenediol di-(meth)-acrylates, polyester di-(meth)-acrylates, divinylbenzene, trivinylbenzene, triallyl cyanurate, allyl (meth)acrylate, butadiene or isoprene.
- Suitable acrylate rubbers are those which contain a crosslinked diene rubber of one or more conjugated dienes and, optionally, an ethylenically unsaturated monomer, such as styrene and/or acrylonitrile, as core.
- Other suitable rubbers are, for example, EPDM rubbers, i.e. rubbers of ethylene, propylene and an unconjugated diene, and also silicone rubbers.
- Preferred rubbers for the production of the graft polymers B) are diene and alkyl acrylate rubbers.
- the rubbers are present in the graft polymers B) in the form of at least partly crosslinked particles having an average particle size from 0.09 to 5 ⁇ m and more especially from 0.1 to 1 ⁇ m.
- the graft polymers B) are produced by radical graft copolymerization of the monomer mixtures defind at the beginning of B.1.1) and B.1.2) in the presence of the rubbers B.2) to be grafted and are all known.
- Preferred production processes for the graft polymers B) are emulsion, solution, bulk or suspension polymerization.
- Particularly preferred graft polymers B) are the so-called ABS polymers.
- Nucleus-substituted styrenes are understood to be nucleus-alkylated styrenes, such as for example p-methyl styrene.
- Copolymers of component C) are often formed as secondary products in the graft polymerization for the production of component B), particularly when large quantities of monomers are grafted onto small quantities of rubber.
- the quantity of copolymer C) to be used in accordance with the invention does not include these secondary graft polymerization products.
- copolymers of component C) are resin-like, thermoplastic and rubber-free.
- Particularly preferred copolymers C) are those of styrene with acrylonitrile and, optionally, with methyl methacrylate, of ⁇ -methyl styrene with acrylonitrile and, optionally, with methyl methacrylate or of styrene and ⁇ -methyl styrene with acrylonitrile and, optionally, with methyl methacrylate.
- thermoplastic copolymer C Particularly preferred ratios by weight in the thermoplastic copolymer C) are 60 to 80% by weight C.1) and 40 to 20% by weight C.2).
- the styrene-acrylonitrile copolymers of component C) are known and may be produced by radical polymerization, more especially by emulsion, suspension, solution or bulk polymerization.
- the copolymers of component C) preferably have molecular weights M (weight average, as determined by light scattering or sedimentation) of from 15,000 to 200,000.
- halogen-free phosphorus compounds of component D) suitable for use in accordance with the invention are generally known (cf. for example Ullmann, Enzyklopadie der ischen Chemie, Vol. 18, pages 301 et seq., 1979; Houben-Weyl, Methoden der Organischen Chemie, Vol. 12/1, page 43; Beilstein, Vol. 6, page 177).
- Phosphorus compounds of component D), formula (I), suitable for use in accordance with the invention are, for example, triphenylphosphate, tricresylphosphate, diphenyl-2-ethyl cresylphosphate, tri-(isopropylphenyl)-phosphate, methylphosphonic acid diphenyl ester, phenyl phosphonic acid diethyl ester, diphenyl cresylphosphate and tributylphosphate.
- the tetrafluoroethylene polymers of component e) suitable for use in accordance with the invention are polymers having fluorine contents of from 65 to 76% by weight and preferably from 70 to 76% by weight.
- Examples of such polymers are polytetrafluoroethylene, tetrafluoroethylene-hexafluoropropylene copolymers or tetrafluoroethylene copolymers containing small quantities of fluorine-free, copolymerizable, ethylenically unsaturated monomers.
- the polymers are known and may be produced by known methods, for example by polymerization of tetrafluoroethylene in aqueous medium with a catalyst forming free radicals, for example sodium, potassium or ammonium peroxydisulfate, under pressures of 7 to 71 kg/cm 2 and at temperatures of from 0° to 200° C. and preferably at temperatures of 20° to 100° C. (For further particulars, cf. for example U.S. Pat. No. 2,393,967.) Depending on the form in which they are used, these materials may have a density of 1.2 to 2.3 g/cm 3 and an average particle size of 0.05 to 1000 ⁇ m.
- a catalyst forming free radicals for example sodium, potassium or ammonium peroxydisulfate
- preferred polytetrafluoroethylenes have average particle sizes from 0.05 to 20 ⁇ m and preferably from 0.08 to 10 ⁇ m and a density of from 1.2 to 1.9 g/cm 3 and are used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) with emulsions of the graft polymers B).
- Suitable tetrafluoroethylene polymers E) useable in powder form have particle sizes of, for example, from 100 to 1000 ⁇ m and densities of 2.0 g/cm 3 to 2.3 g/cm 3 .
- tetrafluoroethylene polymers above all reduces or completely prevents dripping of the molten molding compound in the event of a fire.
- their use in the form of a coagulated mixture improves the surface of moldings produced from the mixtures according to the invention, which is particularly important for the production of moldings of very large surface area and for production at very high processing temperatures.
- an aqueous emulsion (latex) of a graft polymer B) having average latex particle sizes of from 0.1 to 2 ⁇ m and preferably from 0.2 to 0.6 ⁇ m is first mixed with a finely divided emulsion of a tetrafluoroethylene polymer E) in water having average particle sizes of from 0.05 to 20 ⁇ m and more especially from 0.08 to 10 ⁇ m.
- Suitable tetrafluoroethylene polymer emulsions normally have solids contents of from 30 to 70% by weight and more especially from 50 to 60% by weight.
- the emulsions of the graft polymers B) have solids contents of from 25 to 50% by weight and preferably from 30 to 45% by weight.
- the ratio by weight of graft polymer B) to tetrafluoroethylene polymer E) in the emulsion mixture is from 95:5 to 60:40.
- the emulsion mixture is then coagulated in known manner, for example by spray drying, freeze drying or coagulation by addition of inorganic or organic salts, acids, bases or organic water-miscible solvents, such as alcohols, ketones, preferably at temperatures in the range from 20° to 150° C. and more preferably at temperatures in the range from 50° to 100° C. If necessary, the product may be dried at 50° to 200° C. and preferably at 70° to 100° C.
- Suitable tetrafluoroethylene polymer emulsions are commercial products and are marketed, for example, by Dupont as Teflon® 30N.
- thermoplastic molding compounds according to the invention may contain other known additives for polycarbonates, graft polymers or for the thermoplastic polymers, such as stabilizers, pigments, flow aids, mold release agents, fillers and reinforcing materials and/or antistatic agents.
- the filled or reinforced molding compounds may contain up to 60% by weight and preferably from 5 to 50% by weight, based on the filled or reinforced molding compound, of fillers and/or reinforcing materials.
- Suitable reinforcing materials are glass fibers, carbon fibers, aramide fibers, etc.
- Preferred reinforcing materials are glass fibers.
- Preferred fillers which may also have a reinforcing effect are glass beads, mica, silicates, quartz, talcum, titanium dioxide, wollastonite.
- the molding compounds according to the invention consisting of components A), B), D) and E) and, optionally, C) and/or optionally other known additives, such as stabilizers, pigments, flow aids, mold release agents, fillers and reinforcing materials and/or antistatic agents are prepared by mixing the respective constituents in known manner and then melt-compounding or melt-extruding the resulting mixture in standard units, such as internal kneaders or single-screw or twin-screw extruders, at temperatures in the range from 200° to 330° C. or by mixing solutions of the respective components in suitable organic solvents, for example in chlorobenzene, and concentrating the mixed solutions by evaporation in standard evaporation units, for example in evaporation extruders.
- standard units such as internal kneaders or single-screw or twin-screw extruders
- the present invention also relates to a process for the production of thermoplastic molding compounds consisting of components A), B), D) and E) and, optionally, component C), stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents, characterized in that components A), B), D) and E) and, optionally, component C), stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents, are mixed and melt-compounded or melt-extruded in conventional units at temperatures in the range from 200° to 330° C., component E) preferably being used in the form of a coagulated mixture with component B).
- the individual constituents may be mixed in known manner either gradually or at the same time either at around 20° C. (room temperature) or even at a higher temperature.
- the molding compounds according to the present invention may be used for the production of moldings of all kinds.
- moldings may be produced by injection molding.
- Examples of moldings which can be produced from the molding compounds according to the invention include housing components of all kinds, for example for domestic appliances, such as juice presses, coffee machines, mixers, for office machines or cover panels for the building industry and parts for the automotive sector.
- they may be used in the field of electrical engineering where they show very good electrical properties.
- Another form of processing is the production of moldings by deep drawing from prefabricated sheets or films.
- particle size always means the average particle diameter d 50 , as determined by ultracentrifuge measurements in accordance with W. Scholtan et. al., Colloids, u. Z. Polymere 250 (1972), pages 782 to 796.
- Tetrafluoroethylene polymer in the form of a coagulated mixture of an SAN graft polymer emulsion according to B) in water and a tetrafluoroethylene polymer emulsion in water.
- the ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) in the mixture is 90% by weight to 10% by weight.
- the tetrafluoroethylene polymer emulsion has a solids content of 60% by weight; the particle size is between 0.05 and 0.5 ⁇ m.
- the SAN graft polymer emulsion has a solids content of 34% by weight and an average latex particle size of 0.4 ⁇ m.
- the emulsion of the tetrafluoroethylene polymer was mixed with the emulsion of the SAN graft polymer B) and stabilized with 1.8% by weight, based on polymer solids, of phenolic antioxidants. At 85° to 95° C., the mixture was coagulated with an aqueous solution of MgSO 4 (Epsom salt) and acetic acid at pH 4 to 5, filtered and washed until substantially free from electrolyte, subsequently freed from most of the water by centrifugation and then dried at 100° C. to form a powder. This powder may then be compounded with the other components in the described units.
- MgSO 4 Epsom salt
- Components A), B), C), D) and E) were compounded in a Werner & Pfleiderer type ZSK 53 twin-screw extruder at a temperature of 240° C.
- Moldings were produced in an injection molding machine at a temperature of 260° C.
- the fire behavior of the test specimens was measured in accordance with UL-Subj. 94 V in test specimen thicknesses of 1.6 mm.
- the UL-94 test is carried out as follows:
- Material samples are molded into bars measuring 127 ⁇ 12.7 ⁇ 1.6 mm.
- the bars are vertically mounted in such a way that the underneath of the test specimen is situated 304 mm above a strip of bandaging material.
- Each test bar is individually ignited by two successive ignitions of 10 seconds duration, the burning properties are observed after each ignition and the test specimen is then evaluated.
- a Bunsen burner having a 10 mm (3.8 inch) tall blue flame of natural gas with a heat content of 3.73 ⁇ 10 4 kJ/m 3 (1000 BUT per cubic foot) is used to ignite the test specimens.
- the UL-94 V-0 classification encompasses the properties of materials described in the following which have been subjected to the UL-94 test.
- the polycarbonate molding compounds in this class contain no test specimens which burn for longer than 10 seconds after each application of the test flame. They do not show a total flame time of more than 50 s during the two flame applications to each test specimen. They contain no test specimens which burn up completely to the retaining clip fastened to the upper end of the test specimen. They contain no test specimens which ignite the wadding arranged beneath the test specimen through burning droplets or particles. They also contain no test specimens which glow for longer than 30 seconds after removal of the test flame.
- Notched impact strength was determined in accordance with DIN 53 453/ISO R 179 using test bars measuring 50 ⁇ 6 ⁇ 4 mm, the test bars being provided with a 2.7 mm deep V-shaped notch.
- the oriterion used for stress crazing behavior was the reduction in impact strength (as determined on test bars measuring 50 ⁇ 6 ⁇ 4 mm in accordance with DIN 53 453/ISO R 179) after storage in a simulated fuel bath (mixture of 50% by weight toluene and 50% by weight iso-octane) at room temperature, the test specimens having been pre-extended on a circular template.
- the values can be expected to be all the more unfavorable, i.e. the deteriorations in the properties can be expected to be greater, the longer the test specimens are stored in the test bath and the greater the pre-extension ⁇ x (in %).
- n.b. The starting value for non-pre-extended test specimens not exposed to the test bath is n.b. ("not broken") for both Examples.
- the impact strength of the Example according to the invention is reduced to a far lesser extent than in the case of the Comparison Example.
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Abstract
Description
TABLE 1 ______________________________________ Composition and properties of the molding compounds Components Notched impact (parts by weight) strength UL 94 V Example A B C D E [kJ/m.sup.2 ] [1.6 mm] ______________________________________ 1 65 5 15 12 3 10.7 VO (invention) 2 65 -- 20 12 3 3.9 VO (Comparison) ______________________________________
Claims (20)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3819081 | 1988-06-04 | ||
DE3819081A DE3819081A1 (en) | 1988-06-04 | 1988-06-04 | FLAME-RESISTANT, IMPACT TOOL POLYCARBONATE MOLDS |
Publications (1)
Publication Number | Publication Date |
---|---|
US5061745A true US5061745A (en) | 1991-10-29 |
Family
ID=6355881
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/355,957 Expired - Lifetime US5061745A (en) | 1988-06-04 | 1989-05-23 | Flame-retardant, high-impact polycarbonate molding compounds |
Country Status (5)
Country | Link |
---|---|
US (1) | US5061745A (en) |
EP (1) | EP0345522B1 (en) |
JP (1) | JPH0670177B2 (en) |
DE (2) | DE3819081A1 (en) |
ES (1) | ES2120943T3 (en) |
Cited By (121)
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US5219907A (en) * | 1991-09-27 | 1993-06-15 | Basf Aktiengesellschaft | Flameproofed molding composition |
US5266618A (en) * | 1991-05-28 | 1993-11-30 | Denki Kagaku Kogyo Kabushiki Kaisha | Flame-retardant resin composition |
US5272193A (en) * | 1991-07-12 | 1993-12-21 | Bayer Aktiengesellschaft | Thermoplastic polycarbonate moulding compounds with flame-resistant properties |
US5276256A (en) * | 1991-09-27 | 1994-01-04 | Basf Aktiengesellschaft | Flameproofed chlorine-and bromine-free molding composition |
US5276077A (en) * | 1992-06-03 | 1994-01-04 | The Dow Chemical Company | Ignition resistant carbonate polymer blends |
US5364899A (en) * | 1992-01-24 | 1994-11-15 | Denki Kagaku Koguo Kabushiki Kaisha | Flame-retardant resin composition |
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EP0714932A2 (en) * | 1994-12-01 | 1996-06-05 | Cheil Industries Inc. | Flame proof polycarbonate composition |
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AU676590B2 (en) * | 1993-09-08 | 1997-03-13 | Teijin Chemicals Ltd | Resin composition and molded article |
US5627228A (en) * | 1994-05-10 | 1997-05-06 | Daicel Chemical Industries, Ltd. | Flame-retardant resin composition |
US5658974A (en) * | 1994-10-14 | 1997-08-19 | Bayer Ag | Flameproofed, thermoplastic polycarbonate moulding compounds |
US5672645A (en) * | 1993-08-26 | 1997-09-30 | Bayer Ag | Flame resistant polycarbonate/ABS moulding compounds resistant to stress cracking |
US5674924A (en) * | 1995-08-19 | 1997-10-07 | Cheil Industries Inc. | Flameproof thermoplastic resin compositions |
US5723526A (en) * | 1993-09-08 | 1998-03-03 | Teijin Chemicals Ltd | Resin composition and molded article |
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US6083428A (en) * | 1995-03-07 | 2000-07-04 | Asahi Kasei Kogyo Kabushiki Kaisha | Flame-retardant resin composition |
US6096821A (en) * | 1999-04-02 | 2000-08-01 | General Electric Company | Polyphenylene ether resin concentrates |
US6117542A (en) * | 1997-02-17 | 2000-09-12 | Asahi Kasei Kogyo Kabushiki Kaisha | Flame retardant resin composition |
US6127465A (en) * | 1997-09-04 | 2000-10-03 | Idemitsu Petrochemical Co., Ltd. | Polycarbonate resin composition |
KR100278144B1 (en) * | 1998-07-22 | 2001-01-15 | 유현식 | Thermoplastic resin composition |
US6174945B1 (en) | 1999-06-14 | 2001-01-16 | Lg Chemical Ltd. | Halogen-free flameproof thermoplastic molding materials |
US6228149B1 (en) | 1999-01-20 | 2001-05-08 | Patterson Technique, Inc. | Method and apparatus for moving, filtering and ionizing air |
US6258879B1 (en) | 1999-04-02 | 2001-07-10 | General Electric Company | Polyphenylene ether resin concentrates containing organic phosphates |
US6316579B1 (en) | 1997-07-23 | 2001-11-13 | Daicel Chemical Industries, Ltd. | Polycarbonate resin composition containing block copolymer |
US6319432B1 (en) | 1999-06-11 | 2001-11-20 | Albemarle Corporation | Bisphenol-A bis(diphenyl phosphate)-based flame retardant |
US6331584B1 (en) * | 1998-09-29 | 2001-12-18 | Idemitsu Petrochemical Co., Ltd. | Flame-retardant polycarbonate resin composition and its injection moldings |
US6342550B1 (en) | 1999-02-03 | 2002-01-29 | Mitsubishi Engineering Plastics Corporation | Flame-retardent polycarbonate resin composition and a molded product using the same |
US6359043B1 (en) | 1998-09-24 | 2002-03-19 | General Electric Company | Mica as flame retardant in glass filled noryl |
US6399685B1 (en) | 2000-12-11 | 2002-06-04 | Albemarle Corporation | Purification of arylene polyphosphate esters |
US6403683B1 (en) | 1998-08-28 | 2002-06-11 | Teijin Chemicals Ltd | Polycarbonate resin composition and molded article |
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EP0345522A3 (en) | 1990-12-05 |
JPH0670177B2 (en) | 1994-09-07 |
DE58909840D1 (en) | 1998-10-01 |
JPH0232154A (en) | 1990-02-01 |
DE3819081A1 (en) | 1989-12-07 |
ES2120943T3 (en) | 1998-11-16 |
EP0345522B1 (en) | 1998-08-26 |
EP0345522A2 (en) | 1989-12-13 |
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